US2813700A - Even distribution header system - Google Patents

Even distribution header system Download PDF

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US2813700A
US2813700A US451275A US45127554A US2813700A US 2813700 A US2813700 A US 2813700A US 451275 A US451275 A US 451275A US 45127554 A US45127554 A US 45127554A US 2813700 A US2813700 A US 2813700A
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Prior art keywords
header
main
adapters
inlet
outlet
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US451275A
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Jr Hilbert Van Nydeck Schenck
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Raytheon Technologies Corp
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United Aircraft Corp
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02—Header boxes; End plates
    • F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/027—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes
    • F28F9/0275—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes with multiple branch pipes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
    • F22D1/00—Feed-water heaters, i.e. economisers or like preheaters
    • F22D1/02—Feed-water heaters, i.e. economisers or like preheaters with water tubes arranged in the boiler furnace, fire tubes, or flue ways
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0041—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for only one medium being tubes having parts touching each other or tubes assembled in panel form
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00—Heat exchange
    • Y10S165/355—Heat exchange having separate flow passage for two distinct fluids
    • Y10S165/40—Shell enclosed conduit assembly
    • Y10S165/427—Manifold for tube-side fluid, i.e. parallel
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00—Fluid handling
    • Y10T137/8593—Systems
    • Y10T137/87249—Multiple inlet with multiple outlet
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00—Fluid handling
    • Y10T137/8593—Systems
    • Y10T137/87265—Dividing into parallel flow paths with recombining
    • Y10T137/87281—System having plural inlets

Definitions

  • This invention relates to header systems in which fluid is to be distributed from a main duct, or header, into a multiplicity of smaller ducts, or tubes, and more particularly to systems in which this distribution must be carefully controlled such that each small duct or tube receives a specified fraction of the total flow in the main duct or header.
  • An object of this invention is to provide a new and novel method of providing a variable pressure drop in the form of a varying angularity between the main duct and the small tubes.
  • the fluid distribution in a main header with a multiple branch system will be governed by the total or irreversible pressure drop of the fluid as it traverses each possible path in the system. Only when the total pressure drop through any possible path is equal to the total pressure drop through any other possible path will the flow distribution be stable. Under any other circumstance, the fluid flowing through the path of high pressure drop will tend to be impeded by this high resistance and the flow rate will drop. The fluid flowing through the path of low pressure will be accelerated and the flow rate over this path will increase. These processes will occur over all paths until stability, that is, equal pressure drops over all paths, is achieved. Therefore, control of the total pressure loss or drop over all possible paths is necessary to insure that the main header flow distributes the fluid to the branches in a prescribed and desired manner.
  • Another object of this invention is to provide a simpler and more effective method of controlling the total pressure loss or drop through each tube.
  • the fluid will lose pressure as it traverses the main header, that is, feeding the many small tubes.
  • the fluid at the entrance to the main header will have a higher total pressure than the fluid further down along the header.
  • more of the fluid will tend to turn into the branches near the entrance to the main header pipe, and less and less fluid will turn into the tubes at the farther end from the entrance.
  • This is a generally unfavorable situation since in most fluid distribution systems found in heat exchanger headers, it is desired that all branch tubes receive equal flows of fluid.
  • the unfavorable distribution due to friction in the main header .pipe can be corrected by angling each small tube by a specific amount.
  • Patent By manipulating the variation of lead-off angle, other distribution patterns could be obtained. That is, more fluid can be sent into the branches nearest the main pipe entrance, or more fluid can be sent into the farther branches if this were desired.
  • Figure 1 is a side view, partially in section, of a fluidto-gas heat exchanger having angled branch' pipes at entrance and exit.
  • Figure 2 is an-end view of Fig. 1 as seen from the direction of gas flow.
  • This heat exchanger is a finned-tube type of one-pass and cross-flow arrangement, and comprises a main gas flow duct or chamber 3 and a fluid header system 5.
  • the gas flow duct or chamber 3 is formed rectangular in shape having sides 7, top 8 and bottom 9.
  • the sides 7 are also connected by intermediate plates 11 which divide the gas flow duct or chamber 3 into a plurality of passageways or smaller chambers 13. Extending through the gas flow duct from top to bottom are a plurality of fluid flow tubes.
  • These tubes are arranged in six banks, 15, 16, 17, 18, 19 and 20, with thirteen rows, a, b, c, d, f, g, h, i, j, k, l and m, in each bank.
  • the tubes are fixed to the gas flow duct and have fins 22 aflixed thereto in the passageways 13 formed by the intermediate plates 11.
  • the fluid header system 5 has a main inlet header 24 and a main outlet header 26.
  • Each row of fluid flow tubes 15 through 20 is connected at its upper end by an inlet collector tube 28.
  • Fluid inlet header 24 is attached to each inlet connector tube 28 by an inlet header adapter 30.
  • these inlet connector tubes 28 and header adapters 30 have the row letter affixed when a particular inlet connector tube 28 or header adapter 30 is referred to.
  • the first header connector tube is 23a and the header adapter connecting it to the inlet header 24 is 30a.
  • Each row of fluid flow tubes 15 through 20 is connected at its lower end .by an outlet collector tube 32.
  • Fluid outlet header 26 is attached to each outlet collector tube 32 by a header adapter 34.
  • these outlet collector tubes 32 and header adapters 34 have the row letter aflixed when a particular outlet collector tube 32 or header adapter 34 is referred to.
  • the gas passing therethrough enters at the left of gas flow duct or chamber 3 as viewed in Fig. 1 and passes over the surfaces of intermediate plates 11 and fins 22 of the fluid flow tubes therein as well asaround the fluid flow tubes themselves.
  • This gas flow exits from the other end of the gas flow duct or chamber 3..
  • the flow of gas may be directed into the heat exchanger gas flow duct or chamber 3 in any manner desired and it may be collected or exhausted at the other end by any desirable means.
  • the fluid passing through the fluid header system 5 enters the open end of the main inlet header 24 and passes through the header adapters 30 to the inlet connector tubes 28. From the inlet connector tubes 28 the fluid flows through each of the fluid flow tubes to the outlet collector tubes 32. The fluid is then directed to the main outlet header 26 through header adapters 34.
  • each element of fluid entering the open end of the main inlet header 24 at point A must undergo the same total pressure loss or drop through the heat exchanger 1 to the outlet of the main outlet header 26 at point B. It can be seen that each element of fluid passing from the juncture of any inlet connector tube 28 and inlet header adapter 30 traverses the same length of passageway and makes the same number of turns to the juncture 3* of its cooperating outlet collector tube 32 and outlet header adapter 34. Thus, if equal flow over all other paths is established, the additional flow over these paths will not unbalance-the total flow.
  • header 24 As the fluid traverses the main inlet: header 24, it loses total pressure due to friction.
  • the fluid that turns into a header adapter 30 will also have a total pressure loss, however this is proportionate to the angle of turn which the header adapter forms with the main inlet header 24. This means that the total pressure loss or drop along a path from A to any juncture point C through 0 can be divided into two main separate parts. Substituting these two separate losses or drops for the loss or drop in formulae (a) we have:
  • the Ap friction from A to 30a is the smallest
  • the hp friction from A to 30g is of a medium value
  • the hp friction from A to 30m is the largest.
  • the Ap turning A-C in view of the acute angle ma is the highest
  • the Ap turning A-I is of a medium value
  • the Ap turning A-O in view of the large angle am is the lowest. It can be seen here that (1) a low and high value are added (2) two medium values are added and (3) a high and low value are added tending to equalize the pressure drop. While the difierences in length of the header adapters will produce afurther unbalance, this effect can be overcome by simply changing the angularity of the header adapters slightly.
  • each of the inlet header adapters 30 to the main inlet header 24 and the proper angular position of each of the outlet header adapters 34 to the main outlet header 26 can be (1) figured analytically or (2) actually measured until the pressure drop from A to all the junctures C through 0 are equal when the desired flow distribution is obtained.
  • a header system may be built consisting of a main header and a plurality of smaller tubes extending therefrom; (2) a fluid flow can be directed into the main header and the flow in each of the smaller tubes measured; (3) the angularity of each small tube may then be varied with respect to the main header until like flows are obmined.
  • any means desired may be used. For example, if the tubes are brazed or welded to the main header, in order to change the angularity of the tubes to the main header the tubes may be removed and rebrazed or rewelded at a different angular position.
  • an elongated main header having a fluid inlet at one end, and a plurality of header adapters connected to said main header at spaced locations along the length of the latter, said header adapters being connected to said main header at different angles to produce difierent pressure drops in a fluid passing therebetween.
  • each header adapter nearer one end of said row forming an angle with said header of less than each header adapter nearer the other end of said row forming a cone spending angle with said header of more than 90.
  • a main inlet header said main inlet header having an open inlet end, a plurality of inlet header adapters, said inlet header adapters being con nected to said main inlet header along a length of saidmain inlet header, said inlet header adapters being con.- nected to said main inlet header at different angles tt produce a like pressure drop from the open inlet end of said main inlet header to the downstream end of each inadapters.
  • a main inlet header a plurality of inlet header adapters, said inlet header adapters being connected at their upstream ends to said main inlet header at different angles to produce difierent pressure drops in a fluid entering each inlet header adapter, said inlet header adapters being connected at their downstream ends to fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, a main outlet header, a plurality of outlet header adapters, said' outlet header adapters being connected at their downstream ends to said main outlet header at different angles to produce different pressure drops in a fluid leaving.
  • each outlet header adapter said outlet header adapters:
  • a main inlet header said main inlet header having an open inlet end, a plurality of inlet header adapters, said inlet header adapters being connected to said main inlet header along a length of said main inlet header and extending from said main inlet header in a single plane, said inlet header adapters being connected to said main inlet header at different angles to produce a like pressure drop from the open inlet end of said main inlet header to the downstream end of each inlet header adapter with an equal distribution of flow in all inlet header adapters.
  • a main inlet header a plurality of inlet header adapters, said inlet header adapters being connected at their upstream ends to said main inlet header at different angles to produce different pressure drops in a fluid entering each inlet header adapter, said inlet header adapters being connected at their downstream ends each to an inlet connector tube, the inlet connector tubes each being connected to a set of fluid flow tubes, a gas flow.
  • said fluid flow tubes extending through said gas flow chamber, a plurality of outlet collector tubes, an outlet collector tube being connected to the other end of each set of fluid flow tubes connected to an inlet connector tube, a main outlet header, a plurality of outlet header adapters, said outlet header adapters being connected at their down stream ends to said main outlet header at'difierent angles to produce different pressure drops in a fluid leaving each outlet header adapter, said outlet header adapters being connected at their upstream ends each to an outlet collector tube.
  • a main inlet header having an open end, a plurality of inlet header adapters, said inlet header adapters being connected at their upstream ends to said main inlet header at different angles to .produce a like pressure drop from the open end of said main inlet header to the downstream end of each inlet header adapter, said inlet header adapters being connected at their downstream ends to fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, a main outlet header having an open end, a plurality of outlet header adapters, said outlet header adapters being connected at their downstream ends to said main outlet header at different angles to produce a like pressure drop from the upstream end of each outlet header adapter to the open end of said main outlet header, said outlet header adapters being connected at their upstream ends each to the free end of one of the fluid flow tubes.
  • a main inlet header having an open end, a plurality of inlet header adapters, said inlet header adapters being connected at their upstream ends to said main inlet header at different angles to produce alike pressure drop from the open end of said main inlet header to the downstream end of each inlet header adapter, said inlet header adapters being connected at their downstream ends to fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, said gas flow chamber being divided into smaller chambers, a main outlet header having an open end, a plurality of outlet header adapters, said outlet header adapters being connected at their downstream ends to said main outlet header at different angles to produce a like pressure drop from the upstream end of each outlet header adapter to the open end of said main outlet header, said outlet header adapters being connected at their upstream ends each to the free end of one of the fluid flow tubes.
  • a main inlet header having an open end and a closed end, a plurality of inlet header adapters, said inlet header adapters being connected at one end to said main inlet header at different angles, each inlet header adapter nearer said open end of said main inlet header forming an angle with said header of less than 90, each inlet header adapter nearer said closed end of said main inlet header forming a corresponding angle with said header of more than 90, said inlet header adapters being connected at their other ends each to an inlet connector tube, said inlet connector tubes each being connected to a set of fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, a plurality of outlet collector tubes, an outlet collector tube being connected to the other end of each set of fluid flow tubes connected to an inlet connector tube, a main outlet header having an open end, a plurality of outlet header adapters, said outlet header adapters being connected at one end to said main outlet header at difierent angles, said outlet header adapters being connected at their other ends
  • a main fluid inlet header having an open end, a plurality of inlet header adapters, said inlet header adapters being connected at one end to said main inlet header at different angles to produce a like pressure drop from the open end of said main inlet header to the downstream end of each inlet header adapter, said inlet header adapters being connected at their downstream ends to fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, said gas flow chamber being divided into smaller chambers, a main fluid outlet header having an open end, a plurality of outlet header adap'ters,[said outlet header adapters being connected atone end to said main olutlet header at difierenz angles to produce a like pressure drop from the upstream end of each outlet header adapter to'the open end of said main outlet header, said outlet header adapters being connected at their upstream-ends each to the free end of one of the fluid flow tubes, each inlet header adapter nearer the open end 'of said ma-ininlet header
  • a main inlet header having an open end, a plurality of inlet header adapters, said inlet header adapters being connected at one end to said main inlet header at different angles to produce a like pressure drop from the open end of said main inlet header to the downstream end of each inlet header adapter, said inlet header adapters being connected at their downstream ends to fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, said gas flow chamber being divided into smaller chambers, a main outlet header having an open end, a plurality of outlet header adapters, said outlet header adapters being connected at one end to said main outlet header at difierent angles to produce a like pressure drop from the upstream end of each outlet header adapter to the open end of said main outlet header, said outlet header adapters being connected at their upstream ends each to the free end of one of the fluid flow tubes, each outlet header adapter nearer one end of said main outlet header forming an angle with the latter of less than 90, each outlet header adapter nearer the other end of said main outlet
  • a main inlet header having an open end, a plurality of inlet header adapters, said inlet header adapters being connected at one end to said main inlet header at ditferent angles to produce a like pressure drop from the open end of said main inlet header to the downstream end of each inlet header adapter, said inlet header adapters being connected at their downstream ends to fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, said gas flow chamber being divided into smaller chambers, a main outlet header having an open end, a plurality of outlet header adapters, said outlet header adapters being connected at their downstream ends to said main outlet header at different angles to produce a like pressure drop from the upstream end of each outlet header adapter to the open end of said main outlet header, said outlet header adapters being connected at their upstream ends each to the free end of one of the fluid flow tubes, each inlet header adapter nearer the open end of said main inlet header forming an angle of less than 90, each inlet header adapter nearer the other end of said
  • a method of distributing a fluid flowing in a main pipe into a plurality of smaller tubes which consists of first, measuring the flow in each smaller tube, then, varying the angularity of each smaller tube with respect to the main pipe until like flows are obtained.
  • an elongated main header having a fluid inlet at one end thereof, a plurality of inlet header adapters having fluid connections to said main header at spaced locations along a length thereof, said adapters being connected to said main header at difierent angles to produce different pressure drops in a fluid passing therebetween, said angles being measured between said header adapters and an adjacent upstream portion of said main header,

Description

Unite EVEN DISTU'HON HEADER SYSTEM Application August 20, 1954, Serial No. 451,275
14 Claims. (Cl. 257241) This invention relates to header systems in which fluid is to be distributed from a main duct, or header, into a multiplicity of smaller ducts, or tubes, and more particularly to systems in which this distribution must be carefully controlled such that each small duct or tube receives a specified fraction of the total flow in the main duct or header.
An object of this invention is to provide a new and novel method of providing a variable pressure drop in the form of a varying angularity between the main duct and the small tubes. The fluid distribution in a main header with a multiple branch system will be governed by the total or irreversible pressure drop of the fluid as it traverses each possible path in the system. Only when the total pressure drop through any possible path is equal to the total pressure drop through any other possible path will the flow distribution be stable. Under any other circumstance, the fluid flowing through the path of high pressure drop will tend to be impeded by this high resistance and the flow rate will drop. The fluid flowing through the path of low pressure will be accelerated and the flow rate over this path will increase. These processes will occur over all paths until stability, that is, equal pressure drops over all paths, is achieved. Therefore, control of the total pressure loss or drop over all possible paths is necessary to insure that the main header flow distributes the fluid to the branches in a prescribed and desired manner.
Another object of this invention is to provide a simpler and more effective method of controlling the total pressure loss or drop through each tube. When the fluid turns from the main header into a small tube having a very sharp angle, the total pressure drop due to turning is large and, when the lead-off angle is very slight, so that the fluid continues in almost the same direction in the small tube as in the main header, the total pressure drop due to turning is slight.
In an actual header system, the fluid will lose pressure as it traverses the main header, that is, feeding the many small tubes. Thus the fluid at the entrance to the main header will have a higher total pressure than the fluid further down along the header. Unless some secondary pressure drop inducing mechanism is added to the system, more of the fluid will tend to turn into the branches near the entrance to the main header pipe, and less and less fluid will turn into the tubes at the farther end from the entrance. This is a generally unfavorable situation since in most fluid distribution systems found in heat exchanger headers, it is desired that all branch tubes receive equal flows of fluid. The unfavorable distribution due to friction in the main header .pipe can be corrected by angling each small tube by a specific amount. These tubes near the entrance to the main header will have sharp angles and high total pressure drops, while those farthest from the main header entrance will have shallow angles and low total pressure drops. Thus the sum of friction pressure drop and turning pressure drop into each small tube will be the samefor all paths and the flow will be properly distributed.
Patent By manipulating the variation of lead-off angle, other distribution patterns could be obtained. That is, more fluid can be sent into the branches nearest the main pipe entrance, or more fluid can be sent into the farther branches if this were desired.
For a more complete understanding of the invention, reference should be had to the drawings in which:
Figure 1 is a side view, partially in section, of a fluidto-gas heat exchanger having angled branch' pipes at entrance and exit.
Figure 2 is an-end view of Fig. 1 as seen from the direction of gas flow.
Referring to the figures, the invention is shown embodied in a fluid-to-gas heat exchanger 1. This heat exchanger is a finned-tube type of one-pass and cross-flow arrangement, and comprises a main gas flow duct or chamber 3 and a fluid header system 5. The gas flow duct or chamber 3 is formed rectangular in shape having sides 7, top 8 and bottom 9. The sides 7 are also connected by intermediate plates 11 which divide the gas flow duct or chamber 3 into a plurality of passageways or smaller chambers 13. Extending through the gas flow duct from top to bottom are a plurality of fluid flow tubes. These tubes are arranged in six banks, 15, 16, 17, 18, 19 and 20, with thirteen rows, a, b, c, d, f, g, h, i, j, k, l and m, in each bank. The tubes are fixed to the gas flow duct and have fins 22 aflixed thereto in the passageways 13 formed by the intermediate plates 11.
The fluid header system 5 has a main inlet header 24 and a main outlet header 26. Each row of fluid flow tubes 15 through 20 is connected at its upper end by an inlet collector tube 28. Fluid inlet header 24 is attached to each inlet connector tube 28 by an inlet header adapter 30. (In the specification and figures these inlet connector tubes 28 and header adapters 30 have the row letter affixed when a particular inlet connector tube 28 or header adapter 30 is referred to. For example the first header connector tube is 23a and the header adapter connecting it to the inlet header 24 is 30a.) Each row of fluid flow tubes 15 through 20 is connected at its lower end .by an outlet collector tube 32. Fluid outlet header 26 is attached to each outlet collector tube 32 by a header adapter 34. (In the specification and figures these outlet collector tubes 32 and header adapters 34 have the row letter aflixed when a particular outlet collector tube 32 or header adapter 34 is referred to.)
In this heat exchanger arrangement the gas passing therethrough enters at the left of gas flow duct or chamber 3 as viewed in Fig. 1 and passes over the surfaces of intermediate plates 11 and fins 22 of the fluid flow tubes therein as well asaround the fluid flow tubes themselves. This gas flow exits from the other end of the gas flow duct or chamber 3.. The flow of gas may be directed into the heat exchanger gas flow duct or chamber 3 in any manner desired and it may be collected or exhausted at the other end by any desirable means. The fluid passing through the fluid header system 5 enters the open end of the main inlet header 24 and passes through the header adapters 30 to the inlet connector tubes 28. From the inlet connector tubes 28 the fluid flows through each of the fluid flow tubes to the outlet collector tubes 32. The fluid is then directed to the main outlet header 26 through header adapters 34.
If equal flow in all passages through the heat exchanger is desired, each element of fluid entering the open end of the main inlet header 24 at point A must undergo the same total pressure loss or drop through the heat exchanger 1 to the outlet of the main outlet header 26 at point B. It can be seen that each element of fluid passing from the juncture of any inlet connector tube 28 and inlet header adapter 30 traverses the same length of passageway and makes the same number of turns to the juncture 3* of its cooperating outlet collector tube 32 and outlet header adapter 34. Thus, if equal flow over all other paths is established, the additional flow over these paths will not unbalance-the total flow. These other paths consist of (1a) the paths from point A in the main inlet header 24 to each of the junctures G through of the inlet connector tubes and inlet header adapters, and (2a) the paths from the junctures P through BB of the outlet collector tubes and outlet header adapters to point B in the main outlet header 26.
Taking the paths referred'to in item (la) above, if these pressure drops all remained the same the following relationship would follow:
As the fluid traverses the main inlet: header 24, it loses total pressure due to friction. The fluid that turns into a header adapter 30 will also have a total pressure loss, however this is proportionate to the angle of turn which the header adapter forms with the main inlet header 24. This means that the total pressure loss or drop along a path from A to any juncture point C through 0 can be divided into two main separate parts. Substituting these two separate losses or drops for the loss or drop in formulae (a) we have:
(b) (Ap friction A-C-I-Ap turning AC)=(Ap friction A-D-l-Ap turning AD) .=(Ap friction A-O-l-Ap turning A-O) As viewed in Fig. 1 it can be seen that the distance 1 from A to the point where each successive inlet header adapter connects to the main inlet header 24 increases in length thereby having an increasing total pressure loss or drop due to friction between these various points. To bring this pressure loss or drop to a common value when the flow is distributed equally over all paths, another pressure loss or drop has to be added. Since the pressure losses or drops due to friction all increase, the pressure losses or drops to be added must all decrease from A-C to A-O. A proper angular position of inlet header adapters 30a through 30m will provide this additional pressure loss or drop.
Using rows :1, g and m as examples, the Ap friction from A to 30a is the smallest, the hp friction from A to 30g is of a medium value, and the hp friction from A to 30m is the largest. To compensate for this the Ap turning A-C in view of the acute angle ma is the highest, the Ap turning A-I is of a medium value, and the Ap turning A-O in view of the large angle am is the lowest. It can be seen here that (1) a low and high value are added (2) two medium values are added and (3) a high and low value are added tending to equalize the pressure drop. While the difierences in length of the header adapters will produce afurther unbalance, this effect can be overcome by simply changing the angularity of the header adapters slightly.
The paths referred to in item (2a) above operate in an identical manner to the paths in item (1a) except the flow is reversed.
The proper angular position of each of the inlet header adapters 30 to the main inlet header 24 and the proper angular position of each of the outlet header adapters 34 to the main outlet header 26 can be (1) figured analytically or (2) actually measured until the pressure drop from A to all the junctures C through 0 are equal when the desired flow distribution is obtained.
In determining the proper angular position of the header adapters to the main headers the following method can be used: (1) a header system may be built consisting of a main header and a plurality of smaller tubes extending therefrom; (2) a fluid flow can be directed into the main header and the flow in each of the smaller tubes measured; (3) the angularity of each small tube may then be varied with respect to the main header until like flows are obmined.- In changing the angularity of the smaller-tubes any means desired may be used. For example, if the tubes are brazed or welded to the main header, in order to change the angularity of the tubes to the main header the tubes may be removed and rebrazed or rewelded at a different angular position.
It is to be understood that the invention is not limited to the specific embodiment herein illustrated and described, but may be used in other ways without departure from its spirit as defined by the following claims.
a let header adapter with equal flow in all inlet header I claim:
1. In combination, an elongated main header having a fluid inlet at one end, and a plurality of header adapters connected to said main header at spaced locations along the length of the latter, said header adapters being connected to said main header at different angles to produce difierent pressure drops in a fluid passing therebetween.
2. In combination, a main header, and a plurality of header adapters in a row, said header adapters being con-v nected to said main header at different angles to produce different pressure drops in a fluid passing therebetweeu, each header adapter nearer one end of said row forming an angle with said header of less than each header adapter nearer the other end of said row forming a cone spending angle with said header of more than 90.
3. In combination, a main inlet header, said main inlet header having an open inlet end, a plurality of inlet header adapters, said inlet header adapters being con nected to said main inlet header along a length of saidmain inlet header, said inlet header adapters being con.- nected to said main inlet header at different angles tt produce a like pressure drop from the open inlet end of said main inlet header to the downstream end of each inadapters.
4. In combination, a main inlet header, a plurality of inlet header adapters, said inlet header adapters being connected at their upstream ends to said main inlet header at different angles to produce difierent pressure drops in a fluid entering each inlet header adapter, said inlet header adapters being connected at their downstream ends to fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, a main outlet header, a plurality of outlet header adapters, said' outlet header adapters being connected at their downstream ends to said main outlet header at different angles to produce different pressure drops in a fluid leaving.
each outlet header adapter, said outlet header adapters:
being connected at their upstream ends each to the free ends of the fluid flow tubes.
5. In combination, a main inlet header, said main inlet header having an open inlet end, a plurality of inlet header adapters, said inlet header adapters being connected to said main inlet header along a length of said main inlet header and extending from said main inlet header in a single plane, said inlet header adapters being connected to said main inlet header at different angles to produce a like pressure drop from the open inlet end of said main inlet header to the downstream end of each inlet header adapter with an equal distribution of flow in all inlet header adapters.
6. In combination, a main inlet header, a plurality of inlet header adapters, said inlet header adapters being connected at their upstream ends to said main inlet header at different angles to produce different pressure drops in a fluid entering each inlet header adapter, said inlet header adapters being connected at their downstream ends each to an inlet connector tube, the inlet connector tubes each being connected to a set of fluid flow tubes, a gas flow. chamber, said fluid flow tubes extending through said gas flow chamber, a plurality of outlet collector tubes, an outlet collector tube being connected to the other end of each set of fluid flow tubes connected to an inlet connector tube, a main outlet header, a plurality of outlet header adapters, said outlet header adapters being connected at their down stream ends to said main outlet header at'difierent angles to produce different pressure drops in a fluid leaving each outlet header adapter, said outlet header adapters being connected at their upstream ends each to an outlet collector tube.
7. In combination, a main inlet header having an open end, a plurality of inlet header adapters, said inlet header adapters being connected at their upstream ends to said main inlet header at different angles to .produce a like pressure drop from the open end of said main inlet header to the downstream end of each inlet header adapter, said inlet header adapters being connected at their downstream ends to fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, a main outlet header having an open end, a plurality of outlet header adapters, said outlet header adapters being connected at their downstream ends to said main outlet header at different angles to produce a like pressure drop from the upstream end of each outlet header adapter to the open end of said main outlet header, said outlet header adapters being connected at their upstream ends each to the free end of one of the fluid flow tubes.
8. In combination, a main inlet header having an open end, a plurality of inlet header adapters, said inlet header adapters being connected at their upstream ends to said main inlet header at different angles to produce alike pressure drop from the open end of said main inlet header to the downstream end of each inlet header adapter, said inlet header adapters being connected at their downstream ends to fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, said gas flow chamber being divided into smaller chambers, a main outlet header having an open end, a plurality of outlet header adapters, said outlet header adapters being connected at their downstream ends to said main outlet header at different angles to produce a like pressure drop from the upstream end of each outlet header adapter to the open end of said main outlet header, said outlet header adapters being connected at their upstream ends each to the free end of one of the fluid flow tubes.
9. In combination, a main inlet header having an open end and a closed end, a plurality of inlet header adapters, said inlet header adapters being connected at one end to said main inlet header at different angles, each inlet header adapter nearer said open end of said main inlet header forming an angle with said header of less than 90, each inlet header adapter nearer said closed end of said main inlet header forming a corresponding angle with said header of more than 90, said inlet header adapters being connected at their other ends each to an inlet connector tube, said inlet connector tubes each being connected to a set of fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, a plurality of outlet collector tubes, an outlet collector tube being connected to the other end of each set of fluid flow tubes connected to an inlet connector tube, a main outlet header having an open end, a plurality of outlet header adapters, said outlet header adapters being connected at one end to said main outlet header at difierent angles, said outlet header adapters being connected at their other ends each to an outlet collector tube, the angularity of the inlet and outlet header adapters being arranged to produce a like pressure drop from the open end of said main inlet header to the open end of said main outlet header through any path.
10. In combination, a main fluid inlet header having an open end, a plurality of inlet header adapters, said inlet header adapters being connected at one end to said main inlet header at different angles to produce a like pressure drop from the open end of said main inlet header to the downstream end of each inlet header adapter, said inlet header adapters being connected at their downstream ends to fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, said gas flow chamber being divided into smaller chambers, a main fluid outlet header having an open end, a plurality of outlet header adap'ters,[said outlet header adapters being connected atone end to said main olutlet header at difierenz angles to produce a like pressure drop from the upstream end of each outlet header adapter to'the open end of said main outlet header, said outlet header adapters being connected at their upstream-ends each to the free end of one of the fluid flow tubes, each inlet header adapter nearer the open end 'of said ma-ininlet header forming an angle with the latter of less than each inlet header adapter nearer the other end of said main inlet header forming with the latter a corresponding angle of more than 90, the angle formed between each inlet header adapter and its connected inlet header being measured from the upstream portion of said connected inlet header.
11. In combination, a main inlet header having an open end, a plurality of inlet header adapters, said inlet header adapters being connected at one end to said main inlet header at different angles to produce a like pressure drop from the open end of said main inlet header to the downstream end of each inlet header adapter, said inlet header adapters being connected at their downstream ends to fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, said gas flow chamber being divided into smaller chambers, a main outlet header having an open end, a plurality of outlet header adapters, said outlet header adapters being connected at one end to said main outlet header at difierent angles to produce a like pressure drop from the upstream end of each outlet header adapter to the open end of said main outlet header, said outlet header adapters being connected at their upstream ends each to the free end of one of the fluid flow tubes, each outlet header adapter nearer one end of said main outlet header forming an angle with the latter of less than 90, each outlet header adapter nearer the other end of said main outlet header forming with the latter a corresponding angle of more than 90, the angle formed between each outlet header adapter and its connected outlet header being measured from the upstream portion of said connected outlet header.
12. In combination, a main inlet header having an open end, a plurality of inlet header adapters, said inlet header adapters being connected at one end to said main inlet header at ditferent angles to produce a like pressure drop from the open end of said main inlet header to the downstream end of each inlet header adapter, said inlet header adapters being connected at their downstream ends to fluid flow tubes, a gas flow chamber, said fluid flow tubes extending through said gas flow chamber, said gas flow chamber being divided into smaller chambers, a main outlet header having an open end, a plurality of outlet header adapters, said outlet header adapters being connected at their downstream ends to said main outlet header at different angles to produce a like pressure drop from the upstream end of each outlet header adapter to the open end of said main outlet header, said outlet header adapters being connected at their upstream ends each to the free end of one of the fluid flow tubes, each inlet header adapter nearer the open end of said main inlet header forming an angle of less than 90, each inlet header adapter nearer the other end of said mean inlet header forming an angle of more than 90, the angle that each inlet header adapter forms with said main inlet header being measured on the same side of said inlet header adapters, each outlet header adapter nearer the open end of said main outlet header forming an angle of less than 90, each outlet header adapter nearer the other end of said main outlet header forming an angle of more than 90, the angle that each outlet header adapter forms with said main outlet header being measured on the same side of said outlet header adapters.
13. A method of distributing a fluid flowing in a main pipe into a plurality of smaller tubes which consists of first, measuring the flow in each smaller tube, then, varying the angularity of each smaller tube with respect to the main pipe until like flows are obtained.
'14. In combination, an elongated main header having a fluid inlet at one end thereof, a plurality of inlet header adapters having fluid connections to said main header at spaced locations along a length thereof, said adapters being connected to said main header at difierent angles to produce different pressure drops in a fluid passing therebetween, said angles being measured between said header adapters and an adjacent upstream portion of said main header,
0 References Cited in the file of this patent UNITED STATES PATENTS Bach Sept. 21, 1937 FOREIGN PATENTS Germany May 25, 1940 Italy Dec. 20, 1934
US451275A 1954-08-20 1954-08-20 Even distribution header system Expired - Lifetime US2813700A (en)

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3326281A (en) * 1964-05-25 1967-06-20 Tylde Water Board Freezing tank
US3552487A (en) * 1967-11-29 1971-01-05 Idemitsu Petrochemical Co Quenching apparatus for use with thermal cracking system
US4237969A (en) * 1979-05-21 1980-12-09 Southern California Gas Company Heat transfer element to replace electrical heating element
US4277953A (en) * 1979-04-30 1981-07-14 Kramer Daniel E Apparatus and method for distributing volatile refrigerant
US4327058A (en) * 1980-07-08 1982-04-27 Wheelabrator-Frye, Inc. Capillary processing unit
US4811696A (en) * 1988-02-16 1989-03-14 Phillips Petroleum Company Bent tube waste heat steam generator and method
WO1994023259A1 (en) * 1993-03-31 1994-10-13 Contaminant Separations, Inc. Heat exchanger
US20120097266A1 (en) * 2010-10-22 2012-04-26 Applied Materials, Inc. Apparatus for controlling gas distribution using orifice ratio conductance control

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US2093825A (en) * 1936-05-07 1937-09-21 Reconstruction Finance Corp Refrigerating coil

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Publication number Priority date Publication date Assignee Title
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US2093825A (en) * 1936-05-07 1937-09-21 Reconstruction Finance Corp Refrigerating coil

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3326281A (en) * 1964-05-25 1967-06-20 Tylde Water Board Freezing tank
US3552487A (en) * 1967-11-29 1971-01-05 Idemitsu Petrochemical Co Quenching apparatus for use with thermal cracking system
US4277953A (en) * 1979-04-30 1981-07-14 Kramer Daniel E Apparatus and method for distributing volatile refrigerant
US4237969A (en) * 1979-05-21 1980-12-09 Southern California Gas Company Heat transfer element to replace electrical heating element
US4327058A (en) * 1980-07-08 1982-04-27 Wheelabrator-Frye, Inc. Capillary processing unit
US4811696A (en) * 1988-02-16 1989-03-14 Phillips Petroleum Company Bent tube waste heat steam generator and method
WO1994023259A1 (en) * 1993-03-31 1994-10-13 Contaminant Separations, Inc. Heat exchanger
US5452758A (en) * 1993-03-31 1995-09-26 Contaminant Separations, Inc. Heat exchanger
US5590707A (en) * 1993-03-31 1997-01-07 Contaminant Separations, Inc. Heat exchanger
US20120097266A1 (en) * 2010-10-22 2012-04-26 Applied Materials, Inc. Apparatus for controlling gas distribution using orifice ratio conductance control
US8905074B2 (en) * 2010-10-22 2014-12-09 Applied Materials, Inc. Apparatus for controlling gas distribution using orifice ratio conductance control

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